US20030006196A1 - Reduction process - Google Patents

Reduction process Download PDF

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Publication number
US20030006196A1
US20030006196A1 US10/164,054 US16405402A US2003006196A1 US 20030006196 A1 US20030006196 A1 US 20030006196A1 US 16405402 A US16405402 A US 16405402A US 2003006196 A1 US2003006196 A1 US 2003006196A1
Authority
US
United States
Prior art keywords
aluminium
hydroxide
potassium
metals
magnesium
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Abandoned
Application number
US10/164,054
Other languages
English (en)
Inventor
Neil Clarke
Stefan Jafverstrom
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Feralco AB
Original Assignee
Feralco AB
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=20284376&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=US20030006196(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Feralco AB filed Critical Feralco AB
Assigned to FERALCO AB reassignment FERALCO AB ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: CLARKE, NEIL, JAFVERSTROM, STEFAN
Publication of US20030006196A1 publication Critical patent/US20030006196A1/en
Abandoned legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5236Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5236Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
    • C02F1/5245Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents using basic salts, e.g. of aluminium and iron
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5236Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
    • C02F1/5254Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents using magnesium compounds and phosphoric acid for removing ammonia
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/58Treatment of water, waste water, or sewage by removing specified dissolved compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/70Treatment of water, waste water, or sewage by reduction
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/70Treatment of water, waste water, or sewage by reduction
    • C02F1/705Reduction by metals
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/10Inorganic compounds
    • C02F2101/20Heavy metals or heavy metal compounds

Definitions

  • the invention relates to a method of purifying an aqueous solution contaminated by aluminium and less noble metals. More precisely, the invention relates to a method of precipitating heavy metals with aluminium from an aqueous solution thereof, whereby the pH of the solution is raised.
  • by-products are obtained from the surface treatment of aluminium.
  • Representative examples are sludges of mainly aluminium hydroxide, waste sulphuric acids from the removal of coatings In the surface treatment, and aqueous sulphuric acid solutions of aluminium sulphate from the recovery of sulphuric acid in the surface treatment.
  • Spent aluminic catalysts are likewise obtained as aluminium hydroxide and aluminium chloride from the oil cracking industry.
  • Other industries also produce aluminic waste materials, which can leach and pollute the environment.
  • electronic scrap comprises ferrous and non-ferrous metals. These metals include copper, aluminium, iron, nickel, tin, and zinc, as well as small amounts of gold and silver.
  • Aluminium sulphate Is an important component in connection with the purification of drinking water, and the limits for this compound are set with reference to the concentration of heavy metals. This is especially important when waters are required, which must meet food standards. In this connection, chromium can constitute a serious problem if a pure raw material is not used in a purification procedure.
  • a polymeric flocculant is used in order to remove from the polluted water such metals as copper, chromium, cobalt, lead, iron, indium, nickel, cadmium, manganese, zinc, molybdenum, bismuth, and vanadium.
  • Complexes called polyaluminium chloride (PAC) are among the commercial products used for such treatments of water.
  • PAC polyaluminium chloride
  • aluminium sulfate is used as a flocculent, whereby a heavy metal containing floc is also formed for removal.
  • the purpose of the invention is to eliminate or reduce the drawbacks mentioned above by providing a method of precipitating a more noble metal with a less noble metal by means of a redox reaction, whereby non-desired reactions are blocked.
  • the invention is based on a reduction reaction that is performed according to known principles with a less noble metal than the impurities to be treated, the less noble metal being aluminium.
  • the more noble metal impurities such as iron, chromium, nickel, cobalt, copper, and manganese, are reduced from their ionic form to their metallic form.
  • ions of more toxic metals such as zinc, lead, cadmium, mercury, vanadium, and nickel ions, are also reduced in the inventive method. These impurities are subsequently removed in the form of metals. This is performed by means of filtration and/or centrifugation.
  • the amount of metallic aluminium required in order to accomplish the reduction reaction depends on the concentrations the more noble impurities as metal salts.
  • the reaction time must also be taken into consideration, i.e. the longer reaction the more metallic aluminium is consumed.
  • the higher oxidation state of the impurity the more metallic aluminium is consumed in order to accomplish the reduction reaction.
  • 1 mole of an impurity having a valence number of 3 requires 1 mole of aluminium
  • 1 mole of an impurity having a valence number of 2 requires 2 ⁇ 3 mole of aluminium
  • 1 mole of an impurity having a valence number of 1 requires 1 ⁇ 3 mole of aluminium.
  • the double amounts of the theoretical values are used in order to guarantee a complete reduction reaction.
  • aluminium chloride is a commercial product of interest, water will always be hydrolyzed and create problems.
  • the inventive method is especially adapted to the reduction of metals in a partly alkalized aluminium chloride solution.
  • the aluminium chloride is so aggressive that it will attack the metallic aluminium before all the heavy metals have been completely reduced. This problem is especially important with chromium.
  • Representative heavy metals which exhibit biological toxicity when released into the environment include copper, zinc, nickel, tin, lead, cadmium, cobalt, mercury, chromium, manganese, silver, gold, platinum, palladium, vanadium, arsenic, antimony, bismuth, indium, rhodium, ruthenium, technetium, molybdenum, nobium, osmium, iridium, uranium, plutionium, lanthanides, actinides, and mixtures thereof.
  • Metal ions which are especially suitable to be purified from a polluted aqueous aluminium solution by means of the method according to the invention, are ions of silver, mercury, copper, lead, tin, molybdenum, nickel, cadmium, iron, zinc, chromium, manganese, and zirconium.
  • Examples of suitable alkalis in the inventive method are magnesium hydroxide, magnesium carbonate, magnesium oxide, magnesium hydroxide, magnesium carbonate, magnesium oxide, aluminium hydroxide, aluminium oxide, metallic aluminium, sodium hydroxide, sodium carbonate, sodium aluminate, potassium hydroxide, potassium carbonate, potassium oxide, potassium aluminate, potassium magnesium carbonate, and mixtures thereof.
  • the aluminium ion has the largest capacity of hydrolyzing water, hydrogen ions being generated which block an effective purification.
  • an alkali e.g. magnesium hydroxide
  • the aluminium ions will become less aggressive, whereby also chromium is reduced.
  • aluminium ions form large complexes or polymeric compounds by means of hydroxide bridges between the aluminium ions in a polluted water solution that is treated with method according to the invention, such as: 2 ⁇ Al 3 + + 2 ⁇ OH - ⁇ [ ⁇ OH Al Al ⁇ ] 4 + OH ⁇
  • inventive method is also adapted to a polluted aqueous solution with suspended material therein.
  • An alkali in this case magnesium hydroxide, was added to the aluminium chloride solution in a molar ratio magnesium hydroxide/aluminium ions of 0.75. Then metallic aluminium was added in a molar ratio metallic aluminium/chromium ions of 10.
  • the chromium ions could react with a metallic aluminium, the amount of chromium in the solution being reduced from 100 mg/l to 10 mg/l (90%).

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Removal Of Specific Substances (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)
US10/164,054 2001-06-07 2002-06-05 Reduction process Abandoned US20030006196A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
SE0101996-7 1999-12-03
SE0101996A SE522777C2 (sv) 2001-06-07 2001-06-07 Reduktionsprocess

Publications (1)

Publication Number Publication Date
US20030006196A1 true US20030006196A1 (en) 2003-01-09

Family

ID=20284376

Family Applications (1)

Application Number Title Priority Date Filing Date
US10/164,054 Abandoned US20030006196A1 (en) 2001-06-07 2002-06-05 Reduction process

Country Status (4)

Country Link
US (1) US20030006196A1 (fr)
EP (1) EP1264801A3 (fr)
NO (1) NO20022643L (fr)
SE (1) SE522777C2 (fr)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20100189613A1 (en) * 2007-09-17 2010-07-29 Areva Federal Services Llc Process for Removal of Aluminum Oxides from Aqueous Media
US20110024360A1 (en) * 2006-03-03 2011-02-03 Inland Environmental Resources, Inc. Compositions and methods for wastewater treatment

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3939405A (en) * 1974-08-19 1976-02-17 Deere & Company Apparatus and method for making decay rate measurements
US4060410A (en) * 1975-07-07 1977-11-29 Marcel Laszlo Process for removing heavy metals from fluid media
US4136026A (en) * 1977-11-23 1979-01-23 Aluminum Company Of America Caustic solution having controlled dissolved aluminum content
US4950326A (en) * 1989-05-01 1990-08-21 Tektronix, Inc. Process for removal of dissolved copper from solution
US5800716A (en) * 1993-10-21 1998-09-01 Laporte Industries Limited Processes for the treatment of acidic liquors and for the production of commercial products thereby
US5976383A (en) * 1991-04-08 1999-11-02 Romar Technologies, Inc. Recycle process for removing dissolved heavy metals from water with aluminum particles

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3347385A1 (de) * 1983-12-29 1985-07-11 Inovan-Stroebe GmbH & Co KG, 7534 Birkenfeld Verfahren zur behandlung metallhaltiger abwaesser
IL91653A0 (en) * 1988-10-11 1990-04-29 Enthone Waste treatment of metal containing solutions
US5069800A (en) * 1990-08-22 1991-12-03 The United States Of America As Represented By The Secretary Of The Interior Chemical process for the denitrification of water
DE19507066C1 (de) * 1995-03-01 1996-05-02 Lpw Anlagen Gmbh Verfahren zur Abscheidung von Restnickel aus verbrauchten galvanotechnischen Nickel-Bädern

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3939405A (en) * 1974-08-19 1976-02-17 Deere & Company Apparatus and method for making decay rate measurements
US4060410A (en) * 1975-07-07 1977-11-29 Marcel Laszlo Process for removing heavy metals from fluid media
US4136026A (en) * 1977-11-23 1979-01-23 Aluminum Company Of America Caustic solution having controlled dissolved aluminum content
US4950326A (en) * 1989-05-01 1990-08-21 Tektronix, Inc. Process for removal of dissolved copper from solution
US5976383A (en) * 1991-04-08 1999-11-02 Romar Technologies, Inc. Recycle process for removing dissolved heavy metals from water with aluminum particles
US5800716A (en) * 1993-10-21 1998-09-01 Laporte Industries Limited Processes for the treatment of acidic liquors and for the production of commercial products thereby

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20110024360A1 (en) * 2006-03-03 2011-02-03 Inland Environmental Resources, Inc. Compositions and methods for wastewater treatment
US20100189613A1 (en) * 2007-09-17 2010-07-29 Areva Federal Services Llc Process for Removal of Aluminum Oxides from Aqueous Media
US7968067B2 (en) * 2007-09-17 2011-06-28 Areva Federal Services, Llc Process for removal of aluminum oxides from aqueous media
US20110311419A1 (en) * 2007-09-17 2011-12-22 Geniesse Donald Process for Removal of Aluminum Oxides from Aqueous Media

Also Published As

Publication number Publication date
SE522777C2 (sv) 2004-03-09
SE0101996D0 (sv) 2001-06-07
NO20022643D0 (no) 2002-06-05
EP1264801A3 (fr) 2003-10-29
SE0101996L (sv) 2002-12-08
EP1264801A2 (fr) 2002-12-11
NO20022643L (no) 2002-12-09

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Legal Events

Date Code Title Description
AS Assignment

Owner name: FERALCO AB, SWEDEN

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:JAFVERSTROM, STEFAN;CLARKE, NEIL;REEL/FRAME:013262/0306

Effective date: 20020618

STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION